EP0075955B1 - Härtbare Poly(oxyalkylen)-Pfropfpolymere - Google Patents

Härtbare Poly(oxyalkylen)-Pfropfpolymere Download PDF

Info

Publication number
EP0075955B1
EP0075955B1 EP82109025A EP82109025A EP0075955B1 EP 0075955 B1 EP0075955 B1 EP 0075955B1 EP 82109025 A EP82109025 A EP 82109025A EP 82109025 A EP82109025 A EP 82109025A EP 0075955 B1 EP0075955 B1 EP 0075955B1
Authority
EP
European Patent Office
Prior art keywords
oxyalkylene
graft copolymer
poly
acrylamide
weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
EP82109025A
Other languages
English (en)
French (fr)
Other versions
EP0075955A1 (de
Inventor
David Joseph Bartkovitz
George Homer Greene
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Union Carbide Corp
Original Assignee
Union Carbide Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Union Carbide Corp filed Critical Union Carbide Corp
Priority to AT82109025T priority Critical patent/ATE25989T1/de
Publication of EP0075955A1 publication Critical patent/EP0075955A1/de
Application granted granted Critical
Publication of EP0075955B1 publication Critical patent/EP0075955B1/de
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F283/00Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G
    • C08F283/06Macromolecular compounds obtained by polymerising monomers on to polymers provided for in subclass C08G on to polyethers, polyoxymethylenes or polyacetals
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913Rod, strand, filament or fiber
    • Y10T428/2933Coated or with bond, impregnation or core
    • Y10T428/2964Artificial fiber or filament
    • Y10T428/2967Synthetic resin or polymer
    • Y10T428/2969Polyamide, polyimide or polyester

Definitions

  • This invention pertains to graft copolymers and, more particularly, to compounds having N-methylol derivatives of acrylamide grafted onto poly(oxyalkylene) polymers to form graft copolymers which are crosslinkable and to methods for preparing such graft copolymers.
  • Poly(oxyalkylene) compounds including poly-(oxyethylenes), poly(oxypropylenes) and copolymers thereof have many and diverse industrial uses such as treatments for metals, paper, textiles and the like.
  • the poly(oxyalkylene) compounds are readily removed from the surface of the substrate materials during the various treatments employed and its effectiveness is, thus, reduced.
  • modified poly(oxyalkylene) compounds which possess many or all of the properties of the unmodified compounds plus new or improved physical and/or chemical properties such as, for example, providing a more durable coating.
  • a process for preparing graft copolymers of poly(oxyalkylene) compounds with a wide variety of olefins which is reported to substantially re-.za the formation of insoluble homopolymer by-products and produce products having improved and/or modified properties is disclosed in US-A-3,418,354.
  • the method disclosed therein generally involves preparing a mixture of an olefin and a catalytic amount of a peroxide containing a peroxide group linked to a tertiary carbon atom and slowly adding said mixture to a poly(oxyalkylene) compound which is maintained at a temperature high enough to cause the grafting reaction to occur.
  • olefinic compounds are suggested as being applicable for use in the grafting reaction of the invention including organic olefins such as styrene, acrylonitrile, alkyl acrylates, and the like.
  • organic olefins such as styrene, acrylonitrile, alkyl acrylates, and the like.
  • graft copolymers of poly(oxyalkylene) com - pounds disclosed are known to significantly enhance the retentivity thereof to substrates such as textile materials and none of the materials disclosed form graft copolymers which are crosslinkable.
  • graft copolymers consist of polyoxyalkylenes onto which, among various others, N-methylol derivatives of acrylamide are grafted.
  • the polyoxyalkylenes are prepared by copolymerizing a mixture of epoxide compounds, one of which must contain a free carbon-carbon double bond, thus resulting in polyoxyalkylenes containing unsaturated moieties in their branch portions.
  • the purpose of grafting is to render aqueous emulsions of said polyoxyalkylenes more stable.
  • graft copolymers of an N-methylol derivative of acrylamide monomer and a poly(oxyalkylene) having said N-methylol derivative of acrylamide grafted onto poly(oxyalkylene) polymers having the formula: wherein R" is a hydrocarbon radical containing up to 10 carbons and has a valence of a, a is an integer having a value of 1 to 4, R' is a hydrogen atom or a monovalent hydrocarbon radical containing up to 6 carbons, n has a value of 2 to 4 inclusive, and z is an integer having a value of 2 to 800, wherein the polyoxyalkylenes do not contain unsaturated moieties in their branch portions, said N-methylol derivative comprising up to 70 percent by weight of the graft copolymer.
  • Said graft copolymers are crosslinkable and, preferably, film forming.
  • the graft copolymers of the invention are substantially free of insoluble homopolymerized monomer (contains less than 2% by weight of said insoluble homopolymer) and are generally fluids even when up to 70 percent by weight of N-methylol derivative of acrylamide is grafted onto the poly-(oxyalkylene) compound.
  • such graft copolymers have been found to be crosslinkable; to exhibit improved properties such as being more adherent to textile and carpet materials, particularly those made from synthetic fibers, without adversely affecting the ability to adhere other materials to such fibers and for certain applications to exhibit improved lubricity.
  • Graft copolymers of the present invention having a N-methylol derivative of acrylamide grafted onto a poly(oxyalkylene) compound are prepared by a method which comprises adding a N-methylol derivative of acrylamide monomer as hereinafter more fully described and a suitable catalyst to an agitated bath of the poly(oxyalkylene), whereby all of said components are intimately admixed at a temperature at which reaction occurs, and maintaining said temperature until said graft copolymer of acrylamide derivative on poly(alkylene oxide) is obtained.
  • the poly(oxyalkylene) compounds used to make the graft copolymers of the invention are known in the art and have the formula: wherein R" is a hydrocarbon radical containing up to 10 carbon atoms and has a valence of a, a is an integer having a value of 1 to 4, R' is a hydrogen atom or a monovalent hydrocarbon radical containing up to 6 carbon atoms, n has a value of 2 to 4 inclusive, and z is an integer having a value of about 2 to about 800.
  • these compounds contain oxyethylene, oxypropylene, oxybutylene groups or both oxyethylene groups and higher oxyalkylene groups such as oxypropylene and oxybutylene groups, either in random or block distribution in their molecules, and have molecular weights (number average) in the range of 100 to 35,000, and, preferably, in the range of 1,500 to 4,000.
  • poly(oxyalkylene) compounds may be made by processes well known in the art by reacting an alkylene oxide or mixtures of alkylene oxides with water or an aliphatic compound which may be saturated or contain some aliphatic unsaturation, having from one up to as many as four active hydrogen atoms, such as monohyd- roxylic alcohols such as ethanol, propanol, and allyl alcohol; dihydroxylic alcohols such as ethylene glycol and monoethylether of glycerine; trihydroxylic alcohols such as glycerine and trimethylolpropane; and tetrahydroxylic alcohols.
  • monohyd- roxylic alcohols such as ethanol, propanol, and allyl alcohol
  • dihydroxylic alcohols such as ethylene glycol and monoethylether of glycerine
  • trihydroxylic alcohols such as glycerine and trimethylolpropane
  • tetrahydroxylic alcohols such as glycerine and tri
  • the poly(oxyalkylene) products of such reactions will have linear or branched oxyalkylene or mixed oxyalkylene chains, and such chains will terminate with hydroxyl groups. Some or all of these hydroxyl groups may be etherified by reaction with a dialkyl sulfate such as diethyl sulfate.
  • the grafting monomers employed in preparing the copolymers of the present invention are substituted acrylamide monomers having the formula wherein R may be the same or different and is a hydrogen atom or a monovalent hydrocarbon radical containing from 1 to 6 carbon atoms.
  • R may be the same or different and is a hydrogen atom or a monovalent hydrocarbon radical containing from 1 to 6 carbon atoms.
  • These acrylamide derivatives monomers are generally homopolymerizable monomers with a reactive crosslinkable pendant group or groups.
  • Illustrative suitable monomers are methoxymethyl acrylamide, ethoxymethyl acrylamide, N-butoxymethyl acrylamide, allyloxymethyl acrylamide, N-butoxymethylmethacrylamide and preferably, N-methylolacrylamide and N-(iso-butoxymethyl)-acrylamide.
  • a catalyst is employed in the process of the invention which is a free radical initiator (grafting catalyst).
  • grafting catalyst a free radical initiator
  • the choice of such initiator is important but any one of a wide variety of known inorganic or organic free radical initiators may be used.
  • the choice of initiator will generally depend on the particular combination of reactants from which the graft copolymer will be prepared.
  • Suitable initiators are azobisisobutyronitrile; hydroperoxides such as t-butyl hydroperoxide and cumene hydroperoxide; acyl peroxides such as benzoxyl peroxide; peroxides such as t-butyl peroxypivalate, di-t-butyl peroxide, and t-butyl perbenzoate; peroxycarbonates such as diethyl peroxydicarbonate and diisopropyl peroxycarbonate; and persulfates such as potassium and sodium persulfates.
  • Homogeneous graft copolymers of the present invention which are substantially free (contains less than 2 percent by weight) of insoluble homopolymerized acrylamide derivative may be prepared by methods known in the art but preferably are prepared in accordance with the present invention by charging the reactants in two separate feed streams, advantageously in gradual and/or incremental amounts, one of which consists of the grafting monomer and a second consisting of the free radical grafting initiator. Either of the reactants may be mixed with a portion of the poly(oxyalkylene) compound prior to feeding them to the reaction zone which when doing so facilitates the gradual or incremental feeding thereof to the reaction mixture.
  • the amount of acrylamide derivative added to the polymerization reactor zone is not critical and may be varied over a wide range. In general, however, up to 70 percent by weight, and preferably from 1 percent by weight to 50 percent by weight based on the total weight of the final graft copolymer, is charged.
  • the temperatures at which the graft reaction of the present invention may be carried out may vary over a wide range and depend, in general, upon the combination of reactants to be used in the reaction.
  • a temperature sufficient to activate the initiator to about 160°C can be used in the grafting reacting, and preferably, a temperature in the range from 70°C to 100°C.
  • a temperature from about above the freezing point of the solvent to about 65°C may be employed. Reaction temperatures above 160°C lead to gelling of the reaction mixture, and should be avoided.
  • Incremental and/or gradual addition of the two separate reactant feed streams coupled with efficient agitation of the poly(oxyalkylene) compound in the reaction zone constitutes the most important technique for producing the graft copolymers of the present invention.
  • This method is particularly important in large scale or commercial operations, not only for preparing the desired homogeneous graft copolymer, but also to facilitate handling and storage of the monomer and the free radical initiator.
  • the grafting reaction of the invention is preferably carried out in bulk without the use of a solvent.
  • a solvent may be used which is non-reactive and inert to the reactants.
  • Suitable solvents include benzene, toluene, tertiary-butylbenzene, heptane, hexane, or octane, and mixtures thereof, and water.
  • the graft copolymers of this invention provide poly(oxyalkylene) copolymers which are crosslinkable, thus rendering them significantly more retentive to a wide range of substrates including textile fibers and fabrics. Moreover, such graft copolymers have been found to have modified and improved properties which render them more useful than the base poly(oxyalkylene) polymers as lubricants for materials such as metals, textiles, fibers and carpets.
  • graft copolymers of the invention crosslink on exposure to heating at, for example, 100-150°C
  • organic catalysts such as para-toluenesulfonic acid, citric acid, and the like are generally added to accelerate crosslinking.
  • inorganic catalysts such as zinc fluoroborate is advantageous.
  • a 12 liter, three-neck round bottom glass flask fitted with a serum stopper, a motor driven mechanical stirrer, and a condenser was used to carry out the reaction of this example.
  • the condenser top was connected to a nitrogen source and to a bubbler.
  • An initial charge of 3,663 grams of an allyl alcohol started ethylene oxide/propylene oxide (40/60 by weight) methoxy capped poly(oxyalkylene) having a viscosity of 580 mm 2 /s (2700 SUS (seconds Universal Saybolt)) and a molecular weight average number of 3700 was placed in the flask and then swept with nitrogen.
  • thermocouple through the serum stopper in the flask was used to control the electrical input to a heating mantle in which the flask rested.
  • Two stainless steel cylinders suspended from load cells having plastic tubing connected to five metering valves and 1.6 mm (1/16 inch) stainless steel tubing through the serum stopper are used to add reactant feed to the reactor.
  • the tubing was positioned to deliver the monomer reactant into the vortex created by the mechanical stirrer in the polymer charge and the initiator to the periphery of the charge. Both feeds are adjusted to be delivered above the liquid level of the reaction mixture and to drop directly into the reactor, not down the walls.
  • the initial charge of poly(oxyalkylene) was brought to a temperature of 80°C, with stirring.
  • One feed reservoir was used to add an initiator feed of 45.8 grams of 75% t-butyl perbenzoate in mineral oil.
  • the other feed reservoir was used to add a feed of 499.4 grams of N-(iso-butoxymethyl) acrylamide (IBMA) (12% of the total weight of the reaction charge).
  • the initiator was slowly fed to the stirred, heated charge in the reactor for 15 minutes before adding acrylamide monomer to the charge in the reactor and, thereafter, both initiator and monomer were concurrently added through separate feed lines over a period of 60 minutes.
  • the resulting reaction mixture was stirred, while maintaining the temperature at 80°C, for an additional 15 minutes before cooling to ambient temperature.
  • the graft copolymer obtained was a light amber, clear liquid having a Brookfield viscosity at 25°C of 8200 mPa - s (average) at 3, 6, and 12 rpm. Proton NMR analysis of the product showed no unreacted IBMA monomer.
  • Example 2 The procedure of Example 1 was repeated with the exception that the poly(oxyalkylene) was an allyl alcohol started ethylene oxide/propylene oxide (40/60 by weight) polymer having a viscosity of 97 mm 2 /s 450 SUS having a molecular weight (average number) of 1400 and an IBMA charge of 12.5% by weight of the reaction charge was used.
  • the graft copolymer obtained was a clear liquid having a Brookfield Viscosity at 25°C of 1420 mPa - s (average) at 6,12,30, and 60 rpm. The graft copolymer gelled after aging 20 min at 150°C indicating that crosslinking had occurred.
  • the procedure hereinabove described was repeated with the exception that the charge contained 6 percent by weight of IBMA instead of 12-1/2 percent.
  • the resultant copolymer was a clear liquid having a Brookfield ViscositY at 25°C of from 300 to 520 mPa - s at 6, 12, 30, and 60 rpm.
  • the copolymer gelled after aging 20 minutes at 150°C indicating that the copolymer was crosslinkable.
  • a four-neck reaction vessel equipped with a mechanical stirrer, a thermoregulator, two separate addition funnels and a condenser containing a nitrogen inlet was used in this Example.
  • the initial charge of poly(oxyalkylene) was swept with nitrogen for four minutes and then heated, with stirring, to the reaction temperature while maintaining a positive nitrogen pressure on the condenser.
  • a catalyst dissolved in the poly(oxyalkylene) compound was slowly added to the reaction mixture through one of the addition funnels.
  • a solution of the acrylamide derivative monomer reactant in a portion of the poly-(oxyalkylene) was slowly added to the reactor charge through the remaining addition funnel.
  • the reactor charge was stirred to maintain a good vortex and the monomer reactant was added directly in the vortex area.
  • the reaction mixture was heated for an additional period of time with stirring.
  • reaction mixture was stirred for an additional 60 minutes at 150°C.
  • the monomer was added in this run in an amount sufficient to achieve a 5 percent by weight of grafted monomer with a molar ratio of monomer to poly(oxyalkylene) polymer of 0.74:1.
  • the product mixture was vacuum stripped and then cooled for analysis.
  • the final product was a light green, clear liquid which infrared spectrum analysis indicated had a low olefinic content.
  • the copolymer gelled when heated for 40-60 minutes at 150°C indicating that the graft copolymer formed was crosslinkable.
  • a 250 ml three neck round bottom flask equipped with a stirrer was used in this example. To this reactor was charged 120 grams of distilled water, 0.5 grams of sodium bicarbonate, 0.5 grams of sodium sulfite and 0.5 grams of sodium persulfate. After dissolution of the salts was completed by stirring, 15.3 grams (0.0059 moles) of the poly(oxyalkylene) polymer used in Example 2 were added and the resulting solution was cooled to 0° to 5°C. A 48 percent aqueous solution of N-methylolacrylamide containing 7.4 grams (0.034 moles) (28.6 weight percent of the total charge) with 5.0 grams additional water was added dropwise to the reaction mixture over a period of 15 minutes. After addition of all reactants was completed, the reaction mixture was stirred for an additional 45 minutes while maintaining the temperature at 0° to 5°C, and then the reaction mixture was allowed to warm to room temperature.
  • the reaction product was a clear solution which when used as a treatment for polyester fabric was shown to withstand at least 5 water wash cycles using a commercial detergent in a mechanical washing machine.
  • Example 4 The procedure of Example 4 was repeated except that 18.6 weight percent, based on the total charge, of N-methylolacrylamide grafting monomer was used and the poly(oxyalkylene) compound was an ethylene glycol started ethylene oxide/propylene oxide (75/25 by weight) having a viscosity of 1080 mm 2 /s (5000 SUS) and a molecular weight of 5000.
  • the reaction product was a clear solution which when used as a treatment for polyester fabric was shown to withstand at least 5 water wash cycles using a commercial detergent in a mechanical washing machine.
  • R" is a residue of a hydrocarbon radical with up to 10, e.g. 2 to 10 carbon atoms and has a valence of 1, 2, 3 or 4 compounds from which this residue R" is derived may be: monovalent alcohols such as ethanol, propanol, i-propanol, n- and i-butanol and corresponding alcohols with 5, 6 and up to 10 carbon atoms. They may contain unsaturated bonds as in allylalcohol; divalent alcohols with at least 2 carbon atoms e.g. ethylene or propylene glycol, the various butylene glycols and similar glycols with 5, 6 and up to 10 carbon atoms.
  • monovalent alcohols such as ethanol, propanol, i-propanol, n- and i-butanol and corresponding alcohols with 5, 6 and up to 10 carbon atoms. They may contain unsaturated bonds as in allylalcohol; divalent alcohols with at least 2 carbon atoms e.
  • trivalent alcohols in which one OH group is etherified with a lower alkyl group belong into this class of compounds like the monoethylether of glycerine or of trimetholpropane.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Graft Or Block Polymers (AREA)
  • Macromonomer-Based Addition Polymer (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Claims (7)

1. Pfropfcopolymer aus einem substituierten N-Methylolderivat von Acrylamid und Poly(oxy- alkylen), bei welchem das N-Methylolderivat des Acrylamids auf ein Poly(oxyalkylen)polymer mit der Formel
Figure imgb0006
gepfropft ist, worin R" ein aliphatischer Kohlenwasserstoffrest mit bis zu 10 Kohlenstoffatomen und einer Wertigkeit von a ist, a eine ganze Zahl mit einem Wert von 1 bis 4 ist, R' ein Wasserstoffatom oder ein einwertiger aliphatischer Kohlenwasserstoffrest mit bis zu 6 Kohlenstoffatomen ist, n einen Wert von 2 bis 4 hat und n eine ganze Zahl mit einem Wert von 2 bis 800 ist, worin die Polyoxyalkylene keine ungesättigten Teile in ihren verzweigten Abschnitten enthalten und das N-Methylolderivat bis zu 70 Gew.-% des Pfropfcopolymers umfaßt.
2. Pfropfcopolymer nach Anspruch 1, worin dieses zur Folienbildung geeignet ist.
3. Pfropfcopolymer nach anspruch 1, worin die Poly(oxyalkylen)verbindungen hergestellt werden können, indem man ein Alkylenoxid oder Mischungen aus Alkylenoxiden mit einer aliphatischen Verbindung, die gesättigt ist oder in gewissem Grad aliphatische ungesättigte Bindungen enthält, umsetzt.
4. Pfropfcopolymer nach Anspruch 1, worin das substituierte Acrylamid-Pfropfmonomer die Formel
Figure imgb0007
hat, worin R gleich oder verschieden sein kann und ein Wasserstoffatom oder ein einwertiger Kohlenwasserstoffrest mit 1 bis 6 Kohlenstoffatomen ist.
5. Pfropfcopolymer nach Anspruch 1, worin das Pfropfmonomer N-(Isobutoxymethyl)-acrylamid ist.
6. Pfropfcopolymer nach Anspruch 1, worin das Pfropfmonomer N-Methylolacrylamid ist.
7. Pfropfcopolymer nach Anspruch 1, worin dieses zwischen 1 und 50 Gew.-% des Pfropfmonomers, bezogen auf das Gewicht des Copolymers, umfaßt.
EP82109025A 1981-09-30 1982-09-29 Härtbare Poly(oxyalkylen)-Pfropfpolymere Expired EP0075955B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82109025T ATE25989T1 (de) 1981-09-30 1982-09-29 Haertbare poly(oxyalkylen)-pfropfpolymere.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US06/307,211 US4394493A (en) 1981-09-30 1981-09-30 Crosslinkable poly(oxyalkylene) graft copolymers
US307211 1999-05-07

Publications (2)

Publication Number Publication Date
EP0075955A1 EP0075955A1 (de) 1983-04-06
EP0075955B1 true EP0075955B1 (de) 1987-03-18

Family

ID=23188736

Family Applications (1)

Application Number Title Priority Date Filing Date
EP82109025A Expired EP0075955B1 (de) 1981-09-30 1982-09-29 Härtbare Poly(oxyalkylen)-Pfropfpolymere

Country Status (13)

Country Link
US (1) US4394493A (de)
EP (1) EP0075955B1 (de)
JP (1) JPS58101106A (de)
KR (1) KR880001856B1 (de)
AT (1) ATE25989T1 (de)
AU (1) AU548031B2 (de)
BR (1) BR8205659A (de)
CA (1) CA1180480A (de)
DE (1) DE3275724D1 (de)
EG (1) EG16013A (de)
HK (1) HK35688A (de)
PH (1) PH17197A (de)
ZA (1) ZA826549B (de)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4604099A (en) * 1984-01-30 1986-08-05 Ciba-Geigy Corporation Process for printing cellulose-containing textile material with foam-containing reactive dyes and addition of (meth) acrylamide polymers
US4703080A (en) * 1985-04-29 1987-10-27 Desoto, Inc. Aqueous latices having improved coating rheology
EP0317833A1 (de) * 1987-11-23 1989-05-31 Irbit Research + Consulting AG Dichtungselement
US4869728A (en) * 1988-09-19 1989-09-26 Texaco Inc. Motor fuel additive and ORI-inhibited motor fuel composition
US5407728A (en) * 1992-01-30 1995-04-18 Reeves Brothers, Inc. Fabric containing graft polymer thereon
US5486210A (en) * 1992-01-30 1996-01-23 Reeves Brothers, Inc. Air bag fabric containing graft polymer thereon
US7342047B2 (en) * 2004-03-02 2008-03-11 3M Innovative Properties Company Crosslinkable hydrophilic materials from reactive oligomers having pendent unsaturated groups

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2719175A (en) * 1952-11-01 1955-09-27 Eastman Kodak Co Vapor phase preparation of n-substituted acrylamides
BE617230A (de) * 1961-05-05
US3418354A (en) * 1964-12-29 1968-12-24 Union Carbide Corp Process for producing graft copolymers
US3546321A (en) * 1967-02-08 1970-12-08 Hercules Inc Polyether graft copolymers
US3652212A (en) * 1967-04-17 1972-03-28 Deering Milliken Res Corp Multi-step in situ polymer formation to produce fabric having improved soiling characteristics
US3660010A (en) * 1969-12-17 1972-05-02 Nat Starch Chem Corp Treating textiles with soil release agents
US3654244A (en) * 1970-03-16 1972-04-04 Us Agriculture Polymers for soil-release textile finishes
US3799910A (en) * 1970-10-12 1974-03-26 Kansai Paint Co Ltd Compositions of polyol etherified methylol acrylamide monomers
US3950317A (en) * 1973-10-29 1976-04-13 Basf Wyandotte Corporation Process for the preparation of graft copolymer dispersions
DE2442101A1 (de) * 1974-09-03 1976-03-11 Bayer Ag Phosphor- und gegebenenfalls stickstoff-enthaltende polymere
US4094797A (en) * 1977-08-01 1978-06-13 Basf Wyandotte Corporation Oxidation stable fiber lubricant

Also Published As

Publication number Publication date
JPS58101106A (ja) 1983-06-16
BR8205659A (pt) 1983-08-30
KR880001856B1 (ko) 1988-09-22
US4394493A (en) 1983-07-19
DE3275724D1 (en) 1987-04-23
AU8834182A (en) 1983-04-14
HK35688A (en) 1988-05-20
EP0075955A1 (de) 1983-04-06
CA1180480A (en) 1985-01-02
KR840001596A (ko) 1984-05-07
ZA826549B (en) 1983-07-27
ATE25989T1 (de) 1987-04-15
AU548031B2 (en) 1985-11-21
EG16013A (en) 1987-10-30
PH17197A (en) 1984-06-19

Similar Documents

Publication Publication Date Title
US4528334A (en) Carboxylated poly(oxyalkylenes)
US5296627A (en) Ethylenically unsaturated poly(alkyleneoxy) surfactants
US7838603B2 (en) Silicone-containing graft copolymers of blockwise structure
US5162475A (en) Polymerizable surfactant
US3418354A (en) Process for producing graft copolymers
EP0853634B1 (de) Kontrolle des molekulargewichts und der endgruppe von polymeren
CA1133504A (en) Carboxylated polyalkylene oxides
US2686772A (en) N, n-ethyleneureido esters of acrylic and methacrylic acids
JPS61197631A (ja) 分子量分布の狭いポリアルキレンオキシドの製造方法
CN101490119B (zh) 亲水性接枝聚合物
JPS58167606A (ja) ラジカル共重合によるグラフト共重合体の製造方法
US5286800A (en) Olefin graft copolymers prepared using borane-containing olefin backbone polymers
EP0075955B1 (de) Härtbare Poly(oxyalkylen)-Pfropfpolymere
KR20190060986A (ko) 계면 활성제 조성물
KR900003913B1 (ko) 퍼플루오로 알킬비닐중합체의 제조방법
US3321430A (en) Graft polymers and a process for the production of aqueous dispersions thereof
US4760152A (en) Pyrrolidonyl acrylate block polymers
EP0642540B1 (de) Komplexe hydrophobe verbindungen, makromonomere und polymere, die makromonomere enthalten
US4463036A (en) Process for imparting hydrophilicity to fabric
US5109075A (en) Comb-shaped graft copolymers of allyl terminated macromolecular monomers of polyethers
JP4157123B2 (ja) 乳化重合用乳化剤、ポリマーエマルションの製造方法及びポリマーエマルション
EP1123942B1 (de) Amino-Gruppe enthaltender Polymer (Salz) und dessen Herstellungsverfahren
US4250071A (en) Mixture of ammonia and alkoxylated poly-siloxanes and its use as a heat sensitizer
US3449300A (en) Styrene/dialkyl fumarate process
EP0119325B1 (de) Verfahren zur Erhöhung der schmierenden und hydrophilen Eigenschaften von synthetischen Fasern und Textilmaterialien

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): AT BE DE FR GB IT NL SE

17P Request for examination filed

Effective date: 19830506

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE DE FR GB IT NL SE

REF Corresponds to:

Ref document number: 25989

Country of ref document: AT

Date of ref document: 19870415

Kind code of ref document: T

ITF It: translation for a ep patent filed

Owner name: ING. C. GREGORJ S.P.A.

REF Corresponds to:

Ref document number: 3275724

Country of ref document: DE

Date of ref document: 19870423

ET Fr: translation filed
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19890401

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19890929

Ref country code: AT

Effective date: 19890929

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19890930

Ref country code: BE

Effective date: 19890930

BERE Be: lapsed

Owner name: UNION CARBIDE CORP.

Effective date: 19890930

GBPC Gb: european patent ceased through non-payment of renewal fee
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Effective date: 19900531

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19900601

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

EUG Se: european patent has lapsed

Ref document number: 82109025.5

Effective date: 19900521